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Mass transfer to clean bubbles at low turbulent energy dissipation
Experimental gas–liquid mass transfer data from a system where single bubbles are kept stationary by a low turbulence downward liquid flow are compared with predictions from theoretical models which take turbulence into account. The data clearly show that, for the turbulence intensities at play, tur...
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Published in: | Chemical engineering science 2006-02, Vol.61 (4), p.1334-1337 |
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container_title | Chemical engineering science |
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creator | Alves, Sebastião S. Vasconcelos, Jorge M.T. Orvalho, Sandra P. |
description | Experimental gas–liquid mass transfer data from a system where single bubbles are kept stationary by a low turbulence downward liquid flow are compared with predictions from theoretical models which take turbulence into account. The data clearly show that, for the turbulence intensities at play, turbulence does not affect mass transfer. Higbie's equation with contact time
t
e
=
d
/
u
may be used for the calculation of the gas–liquid mass transfer coefficient of clean bubbles in systems with levels of turbulent kinetic energy dissipation of, at least, up to
ε
∼
0.04
m
2
s
-
3
. |
doi_str_mv | 10.1016/j.ces.2005.08.001 |
format | article |
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t
e
=
d
/
u
may be used for the calculation of the gas–liquid mass transfer coefficient of clean bubbles in systems with levels of turbulent kinetic energy dissipation of, at least, up to
ε
∼
0.04
m
2
s
-
3
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t
e
=
d
/
u
may be used for the calculation of the gas–liquid mass transfer coefficient of clean bubbles in systems with levels of turbulent kinetic energy dissipation of, at least, up to
ε
∼
0.04
m
2
s
-
3
.</description><subject>Applied sciences</subject><subject>Bubble</subject><subject>Chemical engineering</subject><subject>Exact sciences and technology</subject><subject>Heat and mass transfer. Packings, plates</subject><subject>Higbie</subject><subject>Mass transfer</subject><subject>Turbulence</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2006</creationdate><recordtype>article</recordtype><recordid>eNp9kD1PwzAQhi0EEqXwA9i8wJZwduI4FhNUfElFLDBbjntFrtKk-BxQ_z2pWomN6XTS876nexi7FJALENXNKvdIuQRQOdQ5gDhiE1HrIitLUMdsAgAmkwrMKTsjWo2r1gIm7P7VEfEUXUdLjDz13LfoOt4MTdMicZd42__wNMRmaLFLHDuMn1u-CERh41Lou3N2snQt4cVhTtnH48P77Dmbvz29zO7mmS9UnTKstGm8L50RCL7URdUUtZeFB1UVzhlpUFZSNUr6qqgAjVYL7QwKDboyzhRTdr3v3cT-a0BKdh3IY9u6DvuBrDRCqVLuQLEHfeyJIi7tJoa1i1srwO5s2ZUdbdmdLQu1HW2NmatDuSPv2uUoxAf6C2qlhFQ77nbP4fjpd8BoyQfsPC5CRJ_sog__XPkF5n1-dQ</recordid><startdate>20060201</startdate><enddate>20060201</enddate><creator>Alves, Sebastião S.</creator><creator>Vasconcelos, Jorge M.T.</creator><creator>Orvalho, Sandra P.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7U5</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>L7M</scope></search><sort><creationdate>20060201</creationdate><title>Mass transfer to clean bubbles at low turbulent energy dissipation</title><author>Alves, Sebastião S. ; Vasconcelos, Jorge M.T. ; Orvalho, Sandra P.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c358t-e679bcc4a91e0c4736b38c23c0563aa929e2625b52c6360e975d7a9e170769a93</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2006</creationdate><topic>Applied sciences</topic><topic>Bubble</topic><topic>Chemical engineering</topic><topic>Exact sciences and technology</topic><topic>Heat and mass transfer. Packings, plates</topic><topic>Higbie</topic><topic>Mass transfer</topic><topic>Turbulence</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Alves, Sebastião S.</creatorcontrib><creatorcontrib>Vasconcelos, Jorge M.T.</creatorcontrib><creatorcontrib>Orvalho, Sandra P.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Alves, Sebastião S.</au><au>Vasconcelos, Jorge M.T.</au><au>Orvalho, Sandra P.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Mass transfer to clean bubbles at low turbulent energy dissipation</atitle><jtitle>Chemical engineering science</jtitle><date>2006-02-01</date><risdate>2006</risdate><volume>61</volume><issue>4</issue><spage>1334</spage><epage>1337</epage><pages>1334-1337</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>Experimental gas–liquid mass transfer data from a system where single bubbles are kept stationary by a low turbulence downward liquid flow are compared with predictions from theoretical models which take turbulence into account. The data clearly show that, for the turbulence intensities at play, turbulence does not affect mass transfer. Higbie's equation with contact time
t
e
=
d
/
u
may be used for the calculation of the gas–liquid mass transfer coefficient of clean bubbles in systems with levels of turbulent kinetic energy dissipation of, at least, up to
ε
∼
0.04
m
2
s
-
3
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language | eng |
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source | ScienceDirect Freedom Collection 2022-2024 |
subjects | Applied sciences Bubble Chemical engineering Exact sciences and technology Heat and mass transfer. Packings, plates Higbie Mass transfer Turbulence |
title | Mass transfer to clean bubbles at low turbulent energy dissipation |
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